2020
DOI: 10.1016/j.applthermaleng.2020.115667
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Thermodynamic and thermoeconomic performance analyses and optimization of a novel power and cooling cogeneration system fueled by low-grade waste heat

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Cited by 27 publications
(8 citation statements)
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“…Due to their low or zero ODP, HCFs, including R245fa, have served as transition working fluids to replace CFCs and HCFCs [16,34]. R245fa is widely employed in actual low-grade thermal energy conversion systems, and has been investigated in recent ejector refrigeration performance studies, such as [35,36]. Although, given their GWPs, HFCs are planned to be phased out globally by 2025-2040 [16,34] according to the Montreal Protocol Kigali agreement and Kyoto Protocol [37,38], different baseline and delayed phase-down periods have been granted to developing and/or high ambient temperature countries, including, for example, India [16] and GCC countries [39,40].…”
Section: Solar-assisted Ejector Space Cooling Systemmentioning
confidence: 99%
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“…Due to their low or zero ODP, HCFs, including R245fa, have served as transition working fluids to replace CFCs and HCFCs [16,34]. R245fa is widely employed in actual low-grade thermal energy conversion systems, and has been investigated in recent ejector refrigeration performance studies, such as [35,36]. Although, given their GWPs, HFCs are planned to be phased out globally by 2025-2040 [16,34] according to the Montreal Protocol Kigali agreement and Kyoto Protocol [37,38], different baseline and delayed phase-down periods have been granted to developing and/or high ambient temperature countries, including, for example, India [16] and GCC countries [39,40].…”
Section: Solar-assisted Ejector Space Cooling Systemmentioning
confidence: 99%
“…Generator refrigerant outlet temperature, T g ( • C) 85 (range of variation: 80−100) [18,20,21,35,48] Evaporator refrigerant outlet temperature, T e ( • C) 10 (range of variation: 5−16) [18,20,21,25,35,48] Minimum temperature difference ( • C) Generator 10 [25,36] Condenser 3 [32] Ejector Primary nozzle exit to throat effective area diameter ratio, D 2 /D 1 (-) 1 1.7 [20,21] Isentropic efficiency coefficient for primary nozzle, η p (-) 0.95 [25,35,47] Isentropic efficiency coefficient from nozzle exit to section y, η py (-) 0.88 (this study, based on [20,35])…”
Section: Refrigeration Sub-systemmentioning
confidence: 99%
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“…From the perspectives of thermodynamics and economics, a novel combined cooling and power cogeneration system driven by geothermal hot water was analyzed and optimized by Akbari Kordlar and Mahmoudi [27], which was a combination of an organic Rankine cycle and an absorption refrigeration cycle. A novel power and cooling cogeneration system was designed by Yu et al [28] with three separate objectives: minimize the total cost of unit exergy, maximize the thermal efficiency and exergy efficiency. Baumgä rtner et al [29] and Jaber et al [30] analyzed and optimized energy systems from aspects of economy and environment.…”
Section: Introductionmentioning
confidence: 99%